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1.发明授权Throat and cone gas injector and gas distribution grid for slurry reactor 失效用于泥浆反应器的喉和锥体气体注入器和气体分配网格
公开(公告)号：US06076810A
公开(公告)日：2000-06-20
申请号：US955130
申请日：1997-10-21
摘要： A gas distribution grid for a slurry reactor includes a plurality of gas injectors horizontally arrayed across, and extending through, an otherwise gas and liquid impervious plate. The injectors have a throat open at both ends, with a gas pressure reducing bore at one end which is the entrance end and with the other end opening into an upward opening cone. Flow diverting means in the injectors prevents slurry solids from entering the throat and being attrited by the high velocity gas jet exiting the bore into the throat. It is preferred that the gas injectors not protrude above the top surface of the grid and flat space is eliminated by means such as angular fillers, to prevent solids accumulation top of the grid. A chamfer may be present at the junction of the bore and throat to prevent unrestricted expansion of the gas jet entering the throat. This is useful for injecting gas into a reactive hydrocarbon synthesis slurry in a slurry reactor, with reduced catalyst attrition and deactivation.
摘要翻译： 用于淤浆反应器的气体分配栅格包括多个气体喷射器，水平地排列在另外的气体和液体不可渗透的板的两个并延伸通过。 注射器在两端都有一个喉部开口，一端的气体减压孔是入口端，另一端开口成一个向上的开口锥体。 注射器中的流动分流装置防止浆料固体进入喉部并被离开孔的高速气体射流磨碎到喉部中。 优选地，气体喷射器不突出在格栅的顶表面上方，并且通过诸如角填料的方式消除平坦空间，以防止网格顶部的固体积聚。 在孔和喉部的接合处可能存在倒角，以防止进入喉部的气体射流的不受限制的膨胀。 这对于将气体注入浆料反应器中的反应性烃合成浆料中是有用的，其具有减少的催化剂消耗和失活。
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2.发明授权Combination gas disengaging downcomer-rejuvenation tube for in-situ slurry catalyst rejuvenation (LAW541) 失效用于原位浆液催化剂复原的组合气体分离降液管 - 复原管（LAW541）
公开(公告)号：US5811468A
公开(公告)日：1998-09-22
申请号：US851865
申请日：1997-05-06
IPC分类号： B01J23/94 , B01J8/22 , B01J8/34 , B01J38/10 , B01J38/48 , B01J38/58 , C07C1/06 , C10G2/00 , C07C27/00
摘要： A reversibly deactivated, particulate catalyst in a hydrocarbon synthesis slurry is rejuvenated by circulating the slurry from a slurry body through (i) a gas disengaging zone to remove gas bubbles from the slurry and increase its density, (iii) a downcomer which feeds the gas reduced, dense slurry into the bottom of a rejuvenating tube and applies a positive hydrostatic pressure to the tube, (iii) a catalyst rejuvenation zone in which a catalyst rejuvenating gas, which also acts as a lift gas, contacts the catalyst in slurry to form a catalyst rejuvenated slurry and, (iv) back into the slurry body. Removing gas bubbles prior to rejuvenation improves the rejuvenation efficiency and the downcomer reduces the amount of rejuvenation gas required to maintain slurry circulation through the tube.
摘要翻译： 在烃合成浆料中的可逆失活的颗粒催化剂通过（i）气体分离区使浆料从浆料体循环以从浆料中除去气泡并增加其密度来再生，（iii）将气体进料的降液管 减少密集的浆料进入回弹管的底部并对管施加正的静水压力，（iii）催化剂再生区，其中也用作提升气体的催化剂再生气与浆料中的催化剂接触形成 催化剂再生浆料，（iv）回到浆料体内。 在复原前去除气泡可提高复原效率，并降低降液管，从而减少维持浆液循环通过管所需的复原气体量。
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3.发明授权
公开(公告)号：US5905094A
公开(公告)日：1999-05-18
申请号：US955131
申请日：1997-10-21
摘要： A slurry hydrocarbon synthesis process with reduced catalyst attrition is achieved by injecting a synthesis gas comprising a mixture of H.sub.2 and CO up into the reactive slurry with a gas distribution grid having gas injectors horizontally arrayed across, and vertically extending through, an otherwise gas and liquid impervious plate. The injectors have a throat with a gas pressure reducing orifice at one end, which is the bottom and gas entrance end, and the other end opening into an open cone in which the uprising gas contacts the slurry. Flow diverting means in the injectors prevents slurry from entering the throat and being attrited. The gas injectors do not protrude above the top surface of the plate and flat space is eliminated by means such as angular fillers, to prevent solids accumulation top of the tray.
摘要翻译： 通过将包含H 2和CO 2的混合物的合成气注入到反应性浆料中，将气体分配栅格水平地排列在气体喷射器上并垂直延伸通过另外的气体和液体来实现具有减少的催化剂磨耗的淤浆烃合成方法 不透水板。 喷射器具有在一端具有气体减压孔的喉部，其是底部和气体入口端，另一端开口成开放锥体，其中起始气体接触浆料。 注射器中的分流装置防止浆料进入喉部并磨损。 气体喷射器不突出在板的顶表面之上，并且平面空间通过诸如角填料的方式消除，以防止固体堆积在托盘顶部。
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4.发明授权Throat and cone gas injector and gas distribution grid for slurry reactor (LAW646) 失效用于泥浆反应器的喉和锥体气体注入器和气体分配网格（LAW646）公开(公告)号：US06199835B1
公开(公告)日：2001-03-13
申请号：US09473514
申请日：1999-12-28
IPC分类号： F26B1710
摘要： A gas distribution grid for a slurry reactor includes a plurality of gas injectors horizontally arrayed across, and extending through, an otherwise gas and liquid impervious plate. The injectors have a throat open at both ends, with a gas pressure reducing bore at one end which is the entrance end and with the other end opening into an upward opening cone. Flow diverting means in the injectors prevents slurry solids from entering the throat and being attrited by the high velocity gas jet exiting the bore into the throat. It is preferred that the gas injectors not protrude above the top surface of the grid and flat space is eliminated by means such as angular fillers, to prevent solids accumulation top of the grid. A chamfer may be present at the junction of the bore and throat to prevent unrestricted expansion of the gas jet entering the throat. This is useful for injecting gas into a reactive hydrocarbon synthesis slurry in a slurry reactor, with reduced catalyst attrition and deactivation.
摘要翻译： 用于淤浆反应器的气体分配栅格包括多个气体喷射器，水平地排列在另外的气体和液体不可渗透的板的两个并延伸通过。 注射器在两端都有一个喉部开口，一端的气体减压孔是入口端，另一端开口成一个向上的开口锥体。 注射器中的流动分流装置防止浆料固体进入喉部并被离开孔的高速气体射流磨碎到喉部中。 优选地，气体喷射器不突出在格栅的顶表面上方，并且通过诸如角填料的方式消除平坦空间，以防止网格顶部的固体积聚。 在孔和喉部的接合处可能存在倒角，以防止进入喉部的气体射流的不受限制的膨胀。 这对于将气体注入浆料反应器中的反应性烃合成浆料中是有用的，其具有减少的催化剂消耗和失活。
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5.发明授权
公开(公告)号：US5821270A
公开(公告)日：1998-10-13
申请号：US850356
申请日：1997-05-02
IPC分类号： B01J23/94 , B01J8/00 , B01J8/22 , B01J38/10 , B01J38/58 , C07B61/00 , C07C1/04 , C07C1/06 , C10G2/00 , C07C27/00
CPC分类号： B01J38/58 , B01J8/005 , B01J8/006 , B01J8/228 , C07C1/066 , C07C2523/75 , Y02P20/584
摘要： A reversibly deactivated hydrocarbon synthesis catalyst in a hydrocarbon synthesis slurry is rejuvenated by successively passing the slurry through at least two rejuvenation stages external of the slurry reactor, each of which comprises a rejuvenation zone followed by an offgas removal zone. This is accomplished by using a lift pipe outside the reactor into which slurry from the reactor is passed and contacts a catalyst rejuvenating gas to partially rejuvenate the catalyst particles and form a rejuvenation offgas. The gas and slurry mixture are passed into a vessel in which the gas is removed from the slurry. Rejuvenation gas is bubbled into the slurry in the vessel to further rejuvenate the catalyst. A gas removing downcomer removes gas from the slurry in the vessel before it is passed back into the reactor. The rejuvenation gas also acts as a lift gas in the lift pipe.
摘要翻译： 在烃合成浆料中可逆失活的烃合成催化剂通过连续使浆料通过浆料反应器外部的至少两个再生阶段而恢复活力，每个回收阶段包括再生区，随后是除气区。 这通过在反应器外部使用提升管来实现，在该反应器中通过反应器的浆料通过该提升管并接触催化剂再生气体以部分地使催化剂颗粒恢复活力并形成复原废气。 将气体和浆料混合物送入从浆液中除去气体的容器中。 将再生气体鼓泡到容器中的浆料中以进一步使催化剂复原。 气体去除降液管在其返回到反应器之前从容器中的浆液中除去气体。 再生气也起到升降气体的作用。
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公开(公告)号：US5252613A
公开(公告)日：1993-10-12
申请号：US992983
申请日：1992-12-18
CPC分类号： C07C1/0465 , B01J8/085 , B01J8/22 , C07C1/066 , B01J2208/00955 , B01J2208/00982
摘要： Catalyst particle distribution and mixing in slurry part of bubble columns is improved by introducing a secondary suspending fluid into the columns at locations within the lower 20% of the vertical height of the column but above the gas distributor normally located at or near the bottom of the columns.
摘要翻译： 通过在柱的垂直高度的较低20％的下方的位置但通常位于或接近底部的气体分配器的上方的位置处将二次悬浮流体引入柱中来改善气泡塔的浆料部分中的催化剂颗粒分布和混合 列。
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7.发明授权
公开(公告)号：US5852061A
公开(公告)日：1998-12-22
申请号：US851867
申请日：1997-05-06
CPC分类号： C07C1/0485 , F25J3/0209 , F25J3/0233 , F25J3/0238 , F25J3/0257 , F25J2215/60 , F25J2220/64 , F25J2245/02 , F25J2260/60
摘要： In a hydrocarbon synthesis process, nitrogen is cryogenically removed from natural gas to produce a synthesis gas feed comprising methane which is substantially free of nitrogen. This feed is converted to a synthesis gas comprising a mixture of H.sub.2 and CO which is substantially free of the HCN and NH.sub.3 hydrocarbon synthesis catalyst deactivating nitrogen species. This reduces the need for rejuvenating the hydrocarbon synthesis catalyst. During the cryogenic separation, C.sub.2+ hydrocarbons are separated from the natural gas and all or a portion of the separated C.sub.2 -C.sub.4 hydrocarbons are added to the methane feed before it is converted into syngas, to increase syngas production. All or a portion of the separated C.sub.2 -C.sub.3 hydrocarbons may be removed as LPG.
摘要翻译： 在烃合成方法中，将氮气从天然气中低温除去以产生包含基本上不含氮的甲烷的合成气进料。 将该进料转化为包含H 2和CO的混合物的合成气，其基本上不含HCN和NH 3烃合成催化剂使氮物质失活。 这减少了对烃合成催化剂进行再生的需要。 在低温分离期间，将C2 +烃与天然气分离，将全部或部分分离的C2-C4烃加入到甲烷进料中，然后再转化为合成气，以提高合成气的产量。 所有或部分分离的C2-C3烃可以作为LPG除去。
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